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chemical thermodynamics of neptunium and plutonium - U.S. ...

chemical thermodynamics of neptunium and plutonium - U.S. ...

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A. Discussion <strong>of</strong> selected references 705[84MUL/GOR]In the course <strong>of</strong> this kinetic work, Mulac et al. measured the redox potential <strong>of</strong> the actinide(VI)/actinide(V)couple by cyclic voltammetry in Na 2 CO 3 aqueous solution forAn = U, Np <strong>and</strong> Pu. The actual Na 2 CO 3 concentration was not clearly reported, but itwas probably 0.05 M. There is no indication <strong>of</strong> the junction potential. For these reasons,this review did not use the data reported in this work. The actinide(VI)/actinide(V)couple was written as AnO 2 (CO 3 ) 4−3 /AnO 2(CO 3 ) 5−3in this publication, which is correctin concentrated Na 2 CO 3 aqueous solution; however, in 0.05 M Na 2 CO 3 aqueoussolution the dissociation <strong>of</strong> the actinide(V) limiting complex should probably not beneglected. A more detailed re-interpretation is given in [98VIT/CAP].[84NAS/CLE]Nash <strong>and</strong> Clevel<strong>and</strong>’s primary aim was to explain, with the help <strong>of</strong> the <strong>thermodynamics</strong><strong>of</strong> fluoride complexation <strong>of</strong> Pu(IV), a <strong>plutonium</strong> solubility as high as 10 −7 Mina groundwater <strong>of</strong> pH = 9.3 that contained 2.7 mM fluoride. Their interest lay also inchecking if temperature variations could have a significant impact on fluoride complexation.They used a solvent extraction technique with the extractant HTTA in benzene at25 ◦ C. In one experimental set, the ionic strength <strong>of</strong> the aqueous solution was kept constantat I = 2 M, maintained by HClO 4 , <strong>and</strong> the 1:1 <strong>and</strong> 1:2 formation constants weredetermined at 1, 7.5, 15 <strong>and</strong> 25 ◦ C. In another experimental set the background electrolytewas a mixture <strong>of</strong> 1 M NaClO 4 <strong>and</strong>1MHClO 4 , <strong>and</strong> the <strong>plutonium</strong> concentrationwas varied by a factor <strong>of</strong> about three. The experimental procedure is satisfactory. Theauthors reported enthalpies <strong>of</strong> the equilibriaPu 4+ + qHF(aq) Å PuF 4−qq + qH + (A.60)for q = 1 <strong>and</strong> 2, from the determinations between 1 <strong>and</strong> 25 ◦ C: r H m (A.60, q =1, I = 2M) =−(3.08 ± 0.32) kJ·mol −1 <strong>and</strong> r H m (A.60, q = 2, I = 2M) =−(14.4 ± 1.8) kJ·mol −1 . The Van’t H<strong>of</strong>f plots ([84NAS/CLE], Figure 2) show aslight scattering <strong>of</strong> the data, especially for the 1:2 complex. Since the authors assigneddifferent uncertainties to each constant, we prefer to use these uncertaintiesin a weighted linear regression according to the outline in Appendix C.3. We obtain r Hm ◦ (A.60, q = 1, I = 2M) =−(3.13 ± 2.15) kJ·mol−1 <strong>and</strong> r Hm ◦ (A.60, q =2, I = 2M) =−(13.4 ± 4.9) kJ·mol −1 . These constants are accepted. We assume thattheir ionic strength dependence is small, <strong>and</strong> that they are also valid at I = 0.The authors corrected the resulting constants to I = 0 by estimating the activitycoefficients. We prefer to use the specific ion interaction equation for this correction,<strong>and</strong> we use the constant determined at 25 ◦ Cin2MH + , as well as the average fromthe three determinations in 1 M H + , in our evaluation <strong>of</strong> log ∗ 10 β1 ◦ (A.60, q = 1) <strong>and</strong>log ∗ 10 β2 ◦ (A.60, q = 2). We assign an uncertainty <strong>of</strong> ±0.20 to all values.[84PER/SAP]This paper reports solubility boundaries with respect to the Pu(IV) concentration inaqueous solution <strong>and</strong> pH. The boundary position, if interpreted with respect to Pu 4+ as

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